EP2868208A1 - Method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species - Google Patents

Method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species Download PDF

Info

Publication number
EP2868208A1
EP2868208A1 EP20130191063 EP13191063A EP2868208A1 EP 2868208 A1 EP2868208 A1 EP 2868208A1 EP 20130191063 EP20130191063 EP 20130191063 EP 13191063 A EP13191063 A EP 13191063A EP 2868208 A1 EP2868208 A1 EP 2868208A1
Authority
EP
European Patent Office
Prior art keywords
vitamin
juice
low
hygroscopic
extract
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP20130191063
Other languages
German (de)
French (fr)
Other versions
EP2868208B1 (en
Inventor
Bernd Bonnländer
Erwin Kriesl
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Plantextrakt GmbH&Co KG
PLANTEXTRAKT GmbH and Co KG
Original Assignee
Plantextrakt GmbH&Co KG
PLANTEXTRAKT GmbH and Co KG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Plantextrakt GmbH&Co KG, PLANTEXTRAKT GmbH and Co KG filed Critical Plantextrakt GmbH&Co KG
Priority to EP13191063.0A priority Critical patent/EP2868208B1/en
Priority to ES13191063T priority patent/ES2730852T3/en
Priority to PT13191063T priority patent/PT2868208T/en
Priority to BR102014025999-6A priority patent/BR102014025999B1/en
Publication of EP2868208A1 publication Critical patent/EP2868208A1/en
Application granted granted Critical
Publication of EP2868208B1 publication Critical patent/EP2868208B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/385Concentrates of non-alcoholic beverages
    • A23L2/39Dry compositions
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/70Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
    • A23L2/84Clarifying or fining of non-alcoholic beverages; Removing unwanted matter using microorganisms or biological material, e.g. enzymes
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/15Vitamins
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/335Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin
    • A61K31/365Lactones
    • A61K31/375Ascorbic acid, i.e. vitamin C; Salts thereof
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12HPASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
    • C12H3/00Methods for reducing the alcohol content of fermented solutions or alcoholic beverage to obtain low alcohol or non-alcoholic beverages
    • C12H3/02Methods for reducing the alcohol content of fermented solutions or alcoholic beverage to obtain low alcohol or non-alcoholic beverages by evaporating

Definitions

  • the present invention refers to a process for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species, i.e. a natural product rich in vitamin C of only natural origin from fruits or vegetable in stable, dried form.
  • Acerola (Malpighia glabra) is a tropical plant producing fruits rich in vitamin C. Also Camu Camu (Myrciaria dubia) is an Amazonian tree producing fruits very rich in vitamin C. Other fruits and vegetables which are rich in vitamin C are rose hip, bell pepper, sea buckthorn, orange, black currant or guava.
  • the fruits, juices and juice concentrates of these plants are commercialized, but have limitations because of their water content and thus low stability as well as ineffective shipping. For these reasons drying of such products is performed by known processes to the experts such as spray, freeze or belt drying. However, these techniques are limited in the case of the described products, mainly because of the high sugar content leading to melting and/or highly hygroscopic products, which are not feasible for food or pharma industry.
  • Classical drying aids like maltodextrines or other carriers do not solve the problem, as the relative content of Vitamin C is reduced if these carriers are added.
  • the object of the present invention is to provide a method for the preparation of a low-hygroscopic, dried powder extract of vitamin C rich fruit or vegetable species which method is easy and effective to be performed on an industrial scale.
  • the biochemical method to remove the sugar contents from the juice is based on a fermentation by adding yeast, preferably of the species Saccharomyces cerevisiae, to the juice.
  • yeast preferably of the species Saccharomyces cerevisiae
  • the sugar contents is fermented to ethanol whereafter the ethanol is removed to get the vitamin C rich wet extract as an intermediate product of the process of the present invention.
  • a concentrated juice is used which is diluted to a solution containing 10 % to 30 %, preferably 20 % of soluble solids.
  • the fermentation time is between 2 and 6 days, preferably between 2 and 4 days and/or the fermentation temperature is between 10°C and 50°C, preferably between 20°C and 30°C. All aforesaid parameters help to preserve the high contents of vitamin C on the one hand and to optimise the yield of the production process according to the invention on the other hand.
  • the fermented solution is centrifuged or filtrated and afterwards as an option being evaporated to a concentration higher than 50 % soluble solids by a process with low thermal input, preferably under vacuum.
  • the ethanol may be removed by evaporation by state of the art concentration techniques with low thermal input, preferably under vacuum.
  • Suitable are devices such as a rising film plate, kettle-type, centrifugal, falling film, thin layer or circulation evaporator and reverse osmosis.
  • a UHT process preferably a direct steam treatment UHT process.
  • vitamin C rich wet extract may be dried to the low hygroscopic powder by spray drying, freeze drying or any other appropriate drying technique.
  • Summing up the present invention describes a process to remove said sugars in such products by fermentation processes, not altering significantly other ingredients in the fruit or vegetable products. So a dried, low-hygroscopic product can be produced offering the enhanced stability of such dry products but having high content of ascorbic acid in such products.
  • the starting material can be of such maturity that the relative content of ascorbic acid is the highest, in case of fruits that is mainly unripe fruits ( Weber et al. "Metabolic and isotopic correlations between D-Glucose, L-Ascorbic acid and L-Tartaric Acid", Isotopes Environ. Health Stud. 1997, 33, 151-155 ).
  • 1 kg of concentrated Acerola fruit juice (28 °Brix) is diluted to 10 % soluble solids.
  • Yeast e.g. of the species Saccharomyces cerevisiae, is added at temperatures around its optimal working conditions depending on the type of yeast used. The parameters are taken from a temperature range of preferably 20-25°C and a storage time of usually 3 days. After analysis of the remaining sugar content in the reaction mixture by an enzymatic test the fermented solution is filtrated or separated.
  • the intermediate product thus obtained is a vitamin C rich wet extract which is concentrated by a rising film plate evaporator as state of the art concentration technique with low thermal input, preferably under vacuum to maintain the ascorbic acid.
  • a concentration usually higher than 50 % soluble solids such extract can be used as it is or dried by techniques known to the experts such as spray drying, freeze drying or other drying techniques and produces a low-hygroscopic powder.
  • Vitamin C becomes clear from the following table 1, in which the non-fermented extract is a spray dried Acerola juice concentrate, which has not been treated with yeast and the fermented extract is that of example 1. Both extracts contain 60 % maltodextrin as spray drying agent. Table 1: sugar and vitamin C content of fermented and non-fermented extract Non-fermented extract Fermented extract Content [%] Vitamin C 13.33 18.98 Fructose 4.29 0.03 Glucose 3.25 0.09 Saccharose 0.01 0.01
  • Yeast e.g. of the species Saccharomyces cerevisiae, is added at temperatures around its optimal working conditions depending on the type of yeast used. The parameters are taken from a temperature range of preferably 20-25°C and a storage time of usually 3 days. After analysis of the remaining sugar content by HPLC or enzymatic tests the fermented solution is separated.
  • the intermediate product thus obtained is a vitamin C rich wet extract which is UHT treated, preferably a direct steam treatment UHT process, to remove ethanol.
  • the resulting extract can be dried by techniques as described in example 1.

Landscapes

  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Nutrition Science (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Zoology (AREA)
  • Genetics & Genomics (AREA)
  • General Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Wood Science & Technology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Animal Behavior & Ethology (AREA)
  • Medicinal Chemistry (AREA)
  • Veterinary Medicine (AREA)
  • Epidemiology (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Mycology (AREA)
  • Public Health (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Preparation Of Fruits And Vegetables (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

A method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species, like Acerola (Malpighia glabra), Camu Camu (Myrciaria dubia) or the like, includes the steps of
- preparing a juice of the species,
- removing at least a part of the sugars contained in the juice by a fermentative process generating an ethanol content in the juice but not altering other ingredients in the juice,
- removing the ethanol content from the juice by treating the residue including the vitamin C contents with a low thermal input process to get a vitamin C rich wet extract as residue including the vitamin C contents, and
- drying the residue to a low-hygroscopic powder.

Description

  • The present invention refers to a process for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species, i.e. a natural product rich in vitamin C of only natural origin from fruits or vegetable in stable, dried form.
  • The background of the invention is to be commented as follows. As concerns food products the market and customers nowadays prefer natural origin substances over chemically synthesized compounds. This requires industrial, economic processes to enrich and stabilize substances from natural sources.
  • Acerola (Malpighia glabra) is a tropical plant producing fruits rich in vitamin C. Also Camu Camu (Myrciaria dubia) is an Amazonian tree producing fruits very rich in vitamin C. Other fruits and vegetables which are rich in vitamin C are rose hip, bell pepper, sea buckthorn, orange, black currant or guava.
  • The fruits, juices and juice concentrates of these plants are commercialized, but have limitations because of their water content and thus low stability as well as ineffective shipping. For these reasons drying of such products is performed by known processes to the experts such as spray, freeze or belt drying. However, these techniques are limited in the case of the described products, mainly because of the high sugar content leading to melting and/or highly hygroscopic products, which are not feasible for food or pharma industry. Classical drying aids like maltodextrines or other carriers do not solve the problem, as the relative content of Vitamin C is reduced if these carriers are added.
  • Now the object of the present invention is to provide a method for the preparation of a low-hygroscopic, dried powder extract of vitamin C rich fruit or vegetable species which method is easy and effective to be performed on an industrial scale.
  • This object is achieved by the method according to the characterising steps of claim 1 which are:
    • preparing a juice of the species,
    • removing at least a part of the sugars contained in the juice by a fermentative process not altering other ingredients in the juice,
    • removing the ethanol content from the juice by treating the residue including the vitamin C contents with a low thermal input process to get a vitamin C rich wet extract as residue including the vitamin C contents, and
    • drying the residue to a low hygroscopic powder.
  • Due to the use of processes to reduce or remove the sugar content in such products by fermentation as is further claimed in the depending claims, the remaining compounds including vitamin C (ascorbic acid) in the fruit or vegetable bases are enhanced linked to the reduction of sugar in the final product.
  • The biochemical method to remove the sugar contents from the juice is based on a fermentation by adding yeast, preferably of the species Saccharomyces cerevisiae, to the juice. Thus the sugar contents is fermented to ethanol whereafter the ethanol is removed to get the vitamin C rich wet extract as an intermediate product of the process of the present invention.
  • Within this alternative embodiment preferably a concentrated juice is used which is diluted to a solution containing 10 % to 30 %, preferably 20 % of soluble solids. Further on the fermentation time is between 2 and 6 days, preferably between 2 and 4 days and/or the fermentation temperature is between 10°C and 50°C, preferably between 20°C and 30°C. All aforesaid parameters help to preserve the high contents of vitamin C on the one hand and to optimise the yield of the production process according to the invention on the other hand.
  • To remove yeast the fermented solution is centrifuged or filtrated and afterwards as an option being evaporated to a concentration higher than 50 % soluble solids by a process with low thermal input, preferably under vacuum.
  • The ethanol may be removed by evaporation by state of the art concentration techniques with low thermal input, preferably under vacuum. Suitable are devices such as a rising film plate, kettle-type, centrifugal, falling film, thin layer or circulation evaporator and reverse osmosis.
  • Without evaporation the removal of the ethanol itself may take place by a UHT process, preferably a direct steam treatment UHT process.
  • Finally the vitamin C rich wet extract may be dried to the low hygroscopic powder by spray drying, freeze drying or any other appropriate drying technique.
  • Summing up the present invention describes a process to remove said sugars in such products by fermentation processes, not altering significantly other ingredients in the fruit or vegetable products. So a dried, low-hygroscopic product can be produced offering the enhanced stability of such dry products but having high content of ascorbic acid in such products.
  • To further facilitate such process the starting material can be of such maturity that the relative content of ascorbic acid is the highest, in case of fruits that is mainly unripe fruits (Weber et al. "Metabolic and isotopic correlations between D-Glucose, L-Ascorbic acid and L-Tartaric Acid", Isotopes Environ. Health Stud. 1997, 33, 151-155).
  • Further aspects and advantages of the invention can be taken by the following description of preferred embodiments. The only drawing in
  • Fig. 1
    shows a diagram of sorption isotherms of a non-fermented and a fermented extract
    Example 1:
  • 1 kg of concentrated Acerola fruit juice (28 °Brix) is diluted to 10 % soluble solids. Yeast, e.g. of the species Saccharomyces cerevisiae, is added at temperatures around its optimal working conditions depending on the type of yeast used. The parameters are taken from a temperature range of preferably 20-25°C and a storage time of usually 3 days. After analysis of the remaining sugar content in the reaction mixture by an enzymatic test the fermented solution is filtrated or separated.
  • The intermediate product thus obtained is a vitamin C rich wet extract which is concentrated by a rising film plate evaporator as state of the art concentration technique with low thermal input, preferably under vacuum to maintain the ascorbic acid. At a concentration usually higher than 50 % soluble solids such extract can be used as it is or dried by techniques known to the experts such as spray drying, freeze drying or other drying techniques and produces a low-hygroscopic powder.
  • The mentioned enrichment of Vitamin C becomes clear from the following table 1, in which the non-fermented extract is a spray dried Acerola juice concentrate, which has not been treated with yeast and the fermented extract is that of example 1. Both extracts contain 60 % maltodextrin as spray drying agent. Table 1: sugar and vitamin C content of fermented and non-fermented extract
    Non-fermented extract Fermented extract
    Content [%]
    Vitamin C 13.33 18.98
    Fructose 4.29 0.03
    Glucose 3.25 0.09
    Saccharose 0.01 0.01
  • Example 2:
  • 1 kg of concentrated organic Acerola fruit juice (50 °Brix) is diluted to 20 % soluble solids. Yeast, e.g. of the species Saccharomyces cerevisiae, is added at temperatures around its optimal working conditions depending on the type of yeast used. The parameters are taken from a temperature range of preferably 20-25°C and a storage time of usually 3 days. After analysis of the remaining sugar content by HPLC or enzymatic tests the fermented solution is separated.
  • The intermediate product thus obtained is a vitamin C rich wet extract which is UHT treated, preferably a direct steam treatment UHT process, to remove ethanol. The resulting extract can be dried by techniques as described in example 1.
  • Product check:
  • To prove the low-hygroscopic properties the extracts obtained as explained above are stored in water saturated atmosphere with different relative humidity. The different relative humidities were adjusted by the saturated salt solutions as they are shown in the following table 2: Table 2: saturated salt solution for adjusting relative humidity
    Salt Relative humidity [%]
    Sodium carbonate 44
    Magnesium carbonate 53
    Sodium chloride 75
    Potassium chloride 84
  • These products obtained by the processes according to the invention do not show any physical changes up to 53 % relative humidity in the powder form. Compared to common extracts containing the same carrier content the extract according to the invention behaves much less hygroscopic, what is shown in Fig. 1 presenting the diagram of according sorption isotherms of the non-fermented and fermented extracts according to table 1. The water absorption of a fermented extract is considerably lower - between 4 and 8 percentage points - throughout the complete range between 40% and 85% of practical values of the relative humidity as compared to a non-fermented extract.

Claims (10)

  1. Method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species, like Acerola (Malpighia glabra), Camu Camu (Myrciaria dubia) or the like, characterized by the steps of
    - preparing a juice of the species,
    - removing at least a part of the sugars contained in the juice by a fermentative process generating an ethanol content in the juice but not altering other ingredients in the juice,
    - removing the ethanol content from the juice by treating the residue including the vitamin C contents with a low thermal input process to get a vitamin C rich wet extract as residue including the vitamin C contents, and
    - drying the residue to a low-hygroscopic powder.
  2. Method according to claim 1, characterized in that for removing the sugar by a biochemical process a yeast is added to the juice to ferment the sugar to ethanol.
  3. Method according to claim 2, characterized in that as juice a concentrated juice is used which is diluted to a solution containing 10 % to 30 %, preferably 20 % of soluble solids.
  4. Method according to claim 2 or 3, characterized in that a yeast of the species Saccharomyces cerevisiae is used.
  5. Method according to one of claims 2 to 4, characterized in that the fermentation time is between 2 and 6 days, preferably between 2 and 4 days and/or the fermentation temperature is between 10°C and 50°C, preferably between 20°C and 30°C.
  6. Method according to one of the preceding claims, characterized in that the ethanol content is removed by evaporation by state of the art concentration techniques with low thermal input, preferably under vacuum.
  7. Method according to claim 6, characterized in that one of the following concentration techniques is used: a rising film plate, kettle-type, centrifugal, falling film, thin layer or circulation evaporator or reverse osmosis.
  8. Method according to one of claims 1 to 5, characterized in that the ethanol is removed by a UHT process, preferably a direct steam treatment UHT process.
  9. Method according to one of the preceding claims, characterized in that the vitamin C rich wet extract is concentrated to a concentration higher than 50 % soluble solids by a process with low thermal input, preferably under vacuum.
  10. Method according to one of the preceding claims, characterized in that the vitamin C rich wet extract is dried to the low hygroscopic powder by spray drying or freeze drying.
EP13191063.0A 2013-10-31 2013-10-31 Method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species Active EP2868208B1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
EP13191063.0A EP2868208B1 (en) 2013-10-31 2013-10-31 Method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species
ES13191063T ES2730852T3 (en) 2013-10-31 2013-10-31 Method for preparing a dried, low hygroscopic extract of a kind of fruit or vegetables rich in vitamin C
PT13191063T PT2868208T (en) 2013-10-31 2013-10-31 Method for the preparation of a low-hygroscopic, dried extract of a vitamin c rich fruit or vegetable species
BR102014025999-6A BR102014025999B1 (en) 2013-10-31 2014-10-17 method for preparing a dry extract

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP13191063.0A EP2868208B1 (en) 2013-10-31 2013-10-31 Method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species

Publications (2)

Publication Number Publication Date
EP2868208A1 true EP2868208A1 (en) 2015-05-06
EP2868208B1 EP2868208B1 (en) 2019-04-17

Family

ID=49517323

Family Applications (1)

Application Number Title Priority Date Filing Date
EP13191063.0A Active EP2868208B1 (en) 2013-10-31 2013-10-31 Method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species

Country Status (4)

Country Link
EP (1) EP2868208B1 (en)
BR (1) BR102014025999B1 (en)
ES (1) ES2730852T3 (en)
PT (1) PT2868208T (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111264804A (en) * 2020-03-03 2020-06-12 华中农业大学 Freeze-dried apple powder with low hygroscopicity and preparation method thereof
CN111700247A (en) * 2020-07-16 2020-09-25 广东青云山药业有限公司 Rosa roxburghii powder rich in vitamin C and preparation method thereof
WO2023117528A1 (en) * 2021-12-21 2023-06-29 Société des Produits Nestlé S.A. Fermented acerola beverage

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3012942A (en) * 1958-11-18 1961-12-12 Nutrilite Products Vitamin c concentrate
US3086915A (en) * 1961-08-07 1963-04-23 Nutrilite Products Non-deliquescent vitamin c concentrate
CH632137A5 (en) * 1978-12-21 1982-09-30 Moor Wem Werbeagentur Process for the preparation of a soft (alcohol-free), reduced-calorie fruit juice beverage, and fruit juice beverage prepared by this process
WO1989007132A1 (en) * 1988-01-27 1989-08-10 Bucher-Guyer Ag Maschinenfabrik Process and device for manufacturing dealcoholized beverages
WO2001003520A1 (en) * 1999-07-08 2001-01-18 Ocean Spray Cranberries, Inc. Juice enriched in beneficial compounds
JP2005154432A (en) * 2003-11-05 2005-06-16 Nichirei Corp Treated material of acerola containing polyphenol and/or vitamin c
WO2007141420A2 (en) * 2006-06-07 2007-12-13 Jean-Louis Terras Method for extracting and processing citrus fruit juice, and composition with high vitamin c content

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3012942A (en) * 1958-11-18 1961-12-12 Nutrilite Products Vitamin c concentrate
US3086915A (en) * 1961-08-07 1963-04-23 Nutrilite Products Non-deliquescent vitamin c concentrate
CH632137A5 (en) * 1978-12-21 1982-09-30 Moor Wem Werbeagentur Process for the preparation of a soft (alcohol-free), reduced-calorie fruit juice beverage, and fruit juice beverage prepared by this process
WO1989007132A1 (en) * 1988-01-27 1989-08-10 Bucher-Guyer Ag Maschinenfabrik Process and device for manufacturing dealcoholized beverages
WO2001003520A1 (en) * 1999-07-08 2001-01-18 Ocean Spray Cranberries, Inc. Juice enriched in beneficial compounds
JP2005154432A (en) * 2003-11-05 2005-06-16 Nichirei Corp Treated material of acerola containing polyphenol and/or vitamin c
WO2007141420A2 (en) * 2006-06-07 2007-12-13 Jean-Louis Terras Method for extracting and processing citrus fruit juice, and composition with high vitamin c content

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
DANIELA FRACASSETTI ET AL: "Ellagic acid derivatives, ellagitannins, proanthocyanidins and other phenolics, vitamin C and antioxidant capacity of two powder products from camu-camu fruit (Myrciaria dubia)", FOOD CHEMISTRY, vol. 139, no. 1-4, 1 August 2013 (2013-08-01), pages 578 - 588, XP055116812, ISSN: 0308-8146, DOI: 10.1016/j.foodchem.2013.01.121 *
MOREIRA G E G ET AL: "Physical properties of spray dried acerola pomace extract as affected by temperature and drying aids", LWT- FOOD SCIENCE AND TECHNOLOGY, ACADEMIC PRESS, UNITED KINGDOM, vol. 42, no. 2, 1 March 2009 (2009-03-01), pages 641 - 645, XP025656567, ISSN: 0023-6438, [retrieved on 20080724], DOI: 10.1016/J.LWT.2008.07.008 *
NANTZ M P ET AL: "Immunity and antioxidant capacity in humans is enhanced by consumption of a dried, encapsulated fruit and vegetable juice concentrate", THE JOURNAL OF NUTRITION, AMERICAN SOCIETY FOR NUTRITION, US, vol. 136, no. 10, 1 January 2006 (2006-01-01), pages 2606 - 2610, XP002581661, ISSN: 0022-3166, [retrieved on 20060309] *
WEBER ET AL.: "Metabolic and isotopic correlations between D-Glucose, L-Ascorbic acid and L-Tartaric Acid", ISOTOPES ENVIRON. HEALTH STUD., vol. 33, 1997, pages 151 - 155

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111264804A (en) * 2020-03-03 2020-06-12 华中农业大学 Freeze-dried apple powder with low hygroscopicity and preparation method thereof
CN111700247A (en) * 2020-07-16 2020-09-25 广东青云山药业有限公司 Rosa roxburghii powder rich in vitamin C and preparation method thereof
CN111700247B (en) * 2020-07-16 2022-04-29 广东青云山药业有限公司 Rosa roxburghii powder rich in vitamin C and preparation method thereof
WO2023117528A1 (en) * 2021-12-21 2023-06-29 Société des Produits Nestlé S.A. Fermented acerola beverage

Also Published As

Publication number Publication date
BR102014025999B1 (en) 2020-10-27
BR102014025999A2 (en) 2016-09-06
EP2868208B1 (en) 2019-04-17
ES2730852T3 (en) 2019-11-13
PT2868208T (en) 2019-06-21

Similar Documents

Publication Publication Date Title
CN103704702A (en) Ginkgo ferment and preparation method thereof
KR101566074B1 (en) Method for manufacturing ginseng slices be dampened of fruit enzyme
CN106722503B (en) Preparation method of blueberry powder
EP2868208B1 (en) Method for the preparation of a low-hygroscopic, dried extract of a vitamin C rich fruit or vegetable species
CN103493958A (en) Low-sugar preserved strawberry
CN104187518A (en) Pickle old brine dry powder
CN103461473A (en) Litchi preservative
CN103462133A (en) Fructose roxburgh rose juice beverage and production method thereof
CN107114643B (en) Red date health concentrated juice and preparation method thereof
CN105614635A (en) Morchell esculenta drink granule and production method thereof
CN104478950A (en) Method for extracting persimmon tannin high in small molecular tannin content from persimmon
AU2017261497B2 (en) Fruit and vegetable product beneficial to cardiovascular health and method for preparing same
CN107467571B (en) Areca nut additive and preparation method thereof, and areca nut product and preparation method thereof
KR101434873B1 (en) Preparation method of Cudrania Tricupspidate Bureau extract using seawater and Cudrania Tricupspidate Bureau extract thereby
CN106867822A (en) A kind of liquor made from sorghum and its brewing method rich in glycopeptide
US20110151078A1 (en) Method for osmotically dewatering a cut fruit
KR20140125204A (en) Method for manufacturing red ginseng slices coated of fruit powder
KR102495635B1 (en) Method manufacture of fermented wild ginseng extract and fermented wild ginseng extract manufactured by the same
CN105767302A (en) Preparation method of camellia nitidissima nectar
US1174248A (en) Process of making tomato extract.
Gonzalez-Toxqui et al. Time and energy reduction on grape dehydration by applying dipping solution on freeze drying process
Zeeshan et al. Preservation through osmotic dehydration
CN104256034A (en) Processing method of preserved red date
CN103815010A (en) Application of gamma-aminobutyric acid (GABA) in delay of organic acid degradation of picked oranges and tangerines
Khosravi et al. Investigation on effect of nano zeolite and potassium permagnate on shelf lie extending and quality of red delicious Apple

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20131031

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

R17P Request for examination filed (corrected)

Effective date: 20151030

RBV Designated contracting states (corrected)

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

17Q First examination report despatched

Effective date: 20170721

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

RIC1 Information provided on ipc code assigned before grant

Ipc: A61K 31/375 20060101ALI20181011BHEP

Ipc: A23L 2/84 20060101ALI20181011BHEP

Ipc: A23L 2/39 20060101AFI20181011BHEP

Ipc: A23L 33/15 20150506ALI20181011BHEP

Ipc: C12G 3/08 20060101ALI20181011BHEP

INTG Intention to grant announced

Effective date: 20181113

RIC1 Information provided on ipc code assigned before grant

Ipc: A23L 33/15 20160101ALI20181011BHEP

Ipc: C12G 3/08 20060101ALI20181011BHEP

Ipc: A23L 2/39 20060101AFI20181011BHEP

Ipc: A23L 2/84 20060101ALI20181011BHEP

Ipc: A61K 31/375 20060101ALI20181011BHEP

RIC1 Information provided on ipc code assigned before grant

Ipc: A23L 33/15 20160101ALI20181011BHEP

Ipc: A23L 2/39 20060101AFI20181011BHEP

Ipc: A61K 31/375 20060101ALI20181011BHEP

Ipc: A23L 2/84 20060101ALI20181011BHEP

Ipc: C12G 3/08 20060101ALI20181011BHEP

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602013053962

Country of ref document: DE

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 1120573

Country of ref document: AT

Kind code of ref document: T

Effective date: 20190515

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: PT

Ref legal event code: SC4A

Ref document number: 2868208

Country of ref document: PT

Date of ref document: 20190621

Kind code of ref document: T

Free format text: AVAILABILITY OF NATIONAL TRANSLATION

Effective date: 20190612

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20190417

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190717

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2730852

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20191113

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: RS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190718

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190717

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190817

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602013053962

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

26N No opposition filed

Effective date: 20200120

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 602013053962

Country of ref document: DE

Owner name: MARTIN BAUER GMBH & CO. KG, DE

Free format text: FORMER OWNER: PLANTEXTRAKT GMBH & CO. KG, 91487 VESTENBERGSGREUTH, DE

Ref country code: DE

Ref legal event code: R082

Ref document number: 602013053962

Country of ref document: DE

Representative=s name: RAU, SCHNECK & HUEBNER PATENTANWAELTE RECHTSAN, DE

REG Reference to a national code

Ref country code: CH

Ref legal event code: PUE

Owner name: MARTIN BAUER GMBH AND CO. KG, DE

Free format text: FORMER OWNER: PLANTEXTRAKT GMBH AND CO. KG, DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191031

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20191031

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191031

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20191031

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191031

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191031

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20131031

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190417

REG Reference to a national code

Ref country code: AT

Ref legal event code: UEP

Ref document number: 1120573

Country of ref document: AT

Kind code of ref document: T

Effective date: 20190417

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20231006

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20231117

Year of fee payment: 11

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: PT

Payment date: 20231024

Year of fee payment: 11

Ref country code: IT

Payment date: 20231031

Year of fee payment: 11

Ref country code: FR

Payment date: 20231023

Year of fee payment: 11

Ref country code: DE

Payment date: 20231219

Year of fee payment: 11

Ref country code: CH

Payment date: 20231102

Year of fee payment: 11

Ref country code: AT

Payment date: 20230920

Year of fee payment: 11